EP0023749A1 - Procédé et appareil pour la préparation d'articles en mousse de polyuréthane flexible - Google Patents

Procédé et appareil pour la préparation d'articles en mousse de polyuréthane flexible Download PDF

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Publication number
EP0023749A1
EP0023749A1 EP80301526A EP80301526A EP0023749A1 EP 0023749 A1 EP0023749 A1 EP 0023749A1 EP 80301526 A EP80301526 A EP 80301526A EP 80301526 A EP80301526 A EP 80301526A EP 0023749 A1 EP0023749 A1 EP 0023749A1
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EP
European Patent Office
Prior art keywords
mould
foam
pressure
weight
flexible
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP80301526A
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German (de)
English (en)
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EP0023749B1 (fr
Inventor
George Woods
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Imperial Chemical Industries Ltd
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Imperial Chemical Industries Ltd
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Publication date
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Application filed by Imperial Chemical Industries Ltd filed Critical Imperial Chemical Industries Ltd
Publication of EP0023749A1 publication Critical patent/EP0023749A1/fr
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72—Polyisocyanates or polyisothiocyanates
    • C08G18/74—Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76—Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664—Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34—Auxiliary operations
    • B29C44/3403—Foaming under special conditions, e.g. in sub-atmospheric pressure, in or on a liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C33/00—Moulds or cores; Details thereof or accessories therefor
    • B29C33/10—Moulds or cores; Details thereof or accessories therefor with incorporated venting means
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C37/00—Component parts, details, accessories or auxiliary operations, not covered by group B29C33/00 or B29C35/00
    • B29C37/006—Degassing moulding material or draining off gas during moulding
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2075/00—Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material

Definitions

  • This invention relates to the manufacture of flexible polyurethane foam articles.
  • a method for the manufacture of a flexible polyurethane foam article which comprises introducing into a mould a flexible polyurethane foam-forming mixture, especially such a mixture based on polymeric MDI (as hereinafter defined) and allowing the mixture to foam under a pressure less than normal atmospheric pressure and set.
  • the invention also includes the polyurethane foam article so produced.
  • flexible polyurethane foam-forming mixture is well understood by the skilled worker in the polyurethanes field and methods for the preparation of these mixtures are fully described in the literature. They involve mixing together a polyisocyanate, a polyol and a blowing agent optionally in the presence of other conventional ingredients such as catalysts, surfactants, modifiers, fillers, plasticisers and pigments. When water is used as the blowing agent it reacts with the isocyanate liberating carbon dioxide and forming a urea linkage.
  • polyurethane will be understood, therefore, to include polymers containing urea as well as urethane groups.
  • Hitherto tolylene diisocyanate has been the preponderantly used isocyanate for flexible polyurethane foam manufacture.
  • TDI Hitherto tolylene diisocyanate
  • MDI diphenylmethane diisocyanate
  • MDI diphenylmethane diisocyanate
  • MDI can be used to make an acceptable flexible foam, for instance, for general upholstery applications.
  • the reduced amount of MDI required in our process to provide sufficient carbon dioxide for "blowing" at reduced pressure enables the production of low cost flexible foams where the required level of polymer cross-linking is obtained by the use of MDI containing a proportion of branched isocyanate.
  • MDI containing a proportion of branched isocyanate are flexible polyurethane foam-forming mixtures based on polymeric MDI.
  • Polymeric MDI is a mixture of methylene bridged polyphenyl polyisocyanates containing diisocyanates and higher functionality polyisocyanates and is obtainable from the phosgenation of a corresponding mixture of polyamines which in turn is obtained by condensing aniline with formaldehyde.
  • the constitution of the polymeric MDI will depend inter alia on the selected ratio of reactants in the aniline/formaldehyde condensation and may be adjusted by distillation or crystallisation of all or part of the isocyanate mixture followed by back-blending with undistilled material of the distillate, which is optionally further purified and/or partially reacted with a polyol to form an isocyanate-ended prepolymer.
  • Polymeric MDI compositions are more fully described in, for example, our British patents 1444192 and 1450660.
  • the mixture of isocyanates normally contains from 5 to 70% by weight of polyisocyanates of functionality greater than two and usually from 20 to 60% by weight of such polyisocyanates.
  • polymeric MDI compositions those containing 50 to 75% by weight of diisocyanate, 10 to 40% by weight of triisocyanate and preferably less than 20% by weight of higher functionality isocyanates.
  • the diisocyanate component of the MDI composition ideally consists of 50 to 80% by weight of the 4,4'-isomer of MDI with 10 to 50% by weight of the 2,4'-isomer and may also contain up to 3% by weight of the 2,2'-isomer of MDI.
  • the diisocyanate may be partially reacted with a polyol of equivalent weight between 250 and 2000.
  • Polyols suitable for preparing the foam-forming mixture are well known to the skilled polyurethanes worker. These include polyesters but polyethers are normally used for flexible foams. They may be mixed with the polyisocyanate, blowing agent and other ingredients in one lot to form the foam-forming mixture or part of the polyol may be pre-reacted with the polyisocyanate to form an isocyanate-ended prepolymer which is then mixed with the remainder of the polyol, the blowing agent and other ingredients immediately before the foam-forming mixture so obtained is introduced into the mould.
  • polymeric MDI compositions which we have found most suitable are mixed with polyol compositions consisting of polyether diols, triols or quadrols, or mixtures thereof, of equivalent weight between 750 and 2000 containing 0.4 to 4.0% by weight of water and usefully minor amounts of suitable catalysts, structure modifying surfactants and flame retardant additives.
  • polyol compositions consisting of polyether diols, triols or quadrols, or mixtures thereof, of equivalent weight between 750 and 2000 containing 0.4 to 4.0% by weight of water and usefully minor amounts of suitable catalysts, structure modifying surfactants and flame retardant additives.
  • These mixtures allow the use of isocyanate indices less than 100, i.e. they allow the use of a stoichometric excess of polyol to give foams of commercially desirable properties.
  • the use of a stoichometric excess of the polyol component results in rapid foam cure and ensures the absence of free volatile isocyanate in the hot freshly made foam on
  • the quantities of the MDI composition and polyether are chosen to give an isocyanate-ended prepolymer having an isocyanate value in the range of from 10 to 30% by weight isocyanate.
  • the polyethers used in the first and second stages may differ in molecular weight and functionality.
  • the pressure under which the foam-forming mixture foams is controlled at less than normal atmospheric pressure and is typically about 0.5 bar. It need not be constant, however, and may vary during the moulding period. The pressure in the mould is reduced normally before any significant foam rise occurs.
  • the optimum pressure profile i.e. the optimum rate of change of pressure during the moulding period, will depend inter alia on the particular foam formulation chosen and will readily be determined by trial. Of necessity the mould will need to be enclosed and connected to a vacuum source. A combination of an evacuated reservoir and vacuum pump will permit rapid removal of air from the mould once the foam-forming ingredients have been introduced and control of the reduced pressure during the foaming process.
  • the capacities of the reservoir and pump will be determined by the size and number of moulds served and on the particular foam-forming mixture used since the rate of gas evolution varies from one foam formulation to another. For example, a MDI based foam tends to evolve more gas than a TDI based foam towards the end of the foam-forming reaction.
  • the evacuated reservoir is a second mould of a plurality of moulds which form part of a moulding plant used for the sequential batch manufacture of flexible foam articles.
  • a method for moulding in sequence flexible polyurethane foam articles by repeating the cycle of steps which comprises introducing a flexible polyurethane foam-forming mixture into a first mould; connecting the first mould to a second mould which contains therein a previously foamed flexible foam article and which is at less than normal atmospheric pressure thereby to reduce the pressure in the first mould to less than normal atmospheric pressure; continuing to maintain the first mould at less than normal atmospheric pressure during foaming using a secondary pressure reducing source; isolating the second mould from the first, venting the second mould and removing therefrom the previously formed flexible foam article; connecting the first mould to the second mould or to a third mould in which.a flexible foam forming mixture has been introduced thereby to reduce the pressure in that second or third mould; and thereafter isolating the first mould from that second or third mould, venting the first mould and removing the moulded article therefrom.
  • Such a process finds particular application in the discontinuous manufacture of flexible slabstock, that is blocks of foam typically measuring 2 x 1 x 1 m 3 .
  • the method of the invention obviates the high velocity and high volume (e.g. 25,000 ft 3 /min) air extraction systems associated with present TDI based slabstock plants as the gaseous effluent from the closed moulds may be exhausted via a rotary suction pump and a simple low capacity absorbent column or scrubbing device without hazard to the operators or contamination of the environment.
  • high velocity and high volume e.g. 25,000 ft 3 /min
  • MDI instead of TDI reduces the volatile isocyanate vapour by a factor of about 500 and the high reactivity of most of the isocyanate groups in the preferred MDI compositions compared with TDI results in extremely low levels of unreacted isocyanate remaining in the hot foam immediately after de-moulding. Further, the use of a polymeric or modified polymeric MDI composition with significant triisocyanate content enables the production of sufficiently cross-linked polymers at low levels of polyisocyanate and water.
  • moulding apparatus for making a flexible foam article which comprises an enclosed sectional mould which has an inlet for the reception of a foam-forming mixture and which is connected to a device for exhausting air or other gas or vapour from the mould, said device being controllable to maintain the pressure in the mould at less than normal atmospheric pressure and on a predetermined pressure profile.
  • sectional mould we mean a mould constituted by a plurality of sections or parts which can be clamped, interlocked or otherwise held firmly together during the moulding process, the mould being opened or dismembered into its component sections or parts to release the moulded article. It is desirable that the sections or parts should be sealable in gas-tight manner to enable precise control and collection of all vapours generated during the foaming reaction and to minimise the use of carbon dioxide blowing to reduce the volume and temperature of the gases produced. In addition the use of vacuum sealed moulds and integral mixing heads removes any hazard from isocyanate vapour as well as reducing the amount of isocyanate required for the blowing reaction.
  • the device for exhausting gas or vapour from the mould may be a vacuum pump or other pressure reducing source but preferably it comprises a reservoir which can be held at less than atmospheric pressure to provide a means for rapid exhaustion of the mould and additionally a vacuum pump for maintaining the pressure in the mould on the predetermined pressure profile.
  • the reservoir is a second mould, the moulds being part of a moulding plant for the sequential manufacture of flexible foam articles.
  • a moulding plant for making in sequence flexible foam articles which comprises a plurality of moulds, each mould having an inlet for the reception of a flexible foam-forming mixture, a vent and an outlet for the exhaustion of air or other gas or vapour from the mould, the outlet being connected through a valve arrangement to a second mould, which itself can be exhausted of gas or vapour, and to a secondary pressure reducing source.
  • enclosed sectional moulds A and B have integral mixing heads 5 and.,4,respectively, which are connected to foam ingredient lines 11 and 12, vents 13 and 14 controlled by valves 6 and 7, and outlets 15 and 16 to which pressure gauges 17 and 18 are attached.
  • Moulds A and B and a rotary vacuum pump 3, which is served by a scrubber 22, are interconnected via outlets 15 and 16 by lines 19, 20 and 21, the moulds being isolatable from each other and from vacuum pump 3 by valves 1, 2 and 8.
  • valves 1 and 8 are opened to connect mould A to vacuum pump 3 and the pressure in A is reduced to a predetermined value which, in this example, is 0.5 bar.
  • a polymeric MDI composition and polyol blend are metered to mixing head 4 and dispensed as a foam-forming mixture into mould B.
  • valve 2 is opened to connect mould B with mould A and with vacuum pump 3 to obtain a rapid reduction in the pressure in mould B to a predetermined value.
  • Precise control of the rate of pressure drop and its final value are obtained by control of valves 1, 2 and 8 using electrical operation monitored and controlled by an electronic microprocessor which keys also the operation of the foam injection system.
  • mould B On completion of foaming, mould B, now full of reacted foam under reduced pressure, is isolated by valve 1 from mould A which is allowed to reach atmospheric pressure via valve 6. ' Foam mix is admitted to mould A and the pressure reduced to a predetermined value by closing valve 6 and operating valves 1, 2 and 8 to an extent determined by monitoring the pressure in mould A. At the end of this cycle air is admitted to mould B via vent 14, the mould is opened and the slab of foam, now substantially free from volatile materials is removed and transferred to a cooling and storage room.
  • the system may be enlarged by the addition of further moulds. This not only increases production capacity but, by connecting several moulds by suitably controlled valve and piping arrangements, rapid and controlled pressure reductions may be obtained in the mould during foaming without the need for very high capacity vacuum pumps and high levels of contaminated exhaust gas.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
EP19800301526 1979-07-02 1980-05-09 Procédé et appareil pour la préparation d'articles en mousse de polyuréthane flexible Expired EP0023749B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB7922988 1979-07-02
GB7922988 1979-07-02

Publications (2)

Publication Number Publication Date
EP0023749A1 true EP0023749A1 (fr) 1981-02-11
EP0023749B1 EP0023749B1 (fr) 1983-07-06

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ID=10506248

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EP19800301526 Expired EP0023749B1 (fr) 1979-07-02 1980-05-09 Procédé et appareil pour la préparation d'articles en mousse de polyuréthane flexible

Country Status (3)

Country Link
EP (1) EP0023749B1 (fr)
DE (1) DE3064017D1 (fr)
ES (1) ES492994A0 (fr)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0044226A1 (fr) * 1980-07-15 1982-01-20 Brian James Blackwell Procédé de préparation de matière plastique en mousse
EP0604595A4 (fr) * 1992-01-09 1995-05-10 Scott Carson Procede et dispositif servant a fabriquer des articles en polyurethane.
DE19701728A1 (de) * 1997-01-20 1998-07-23 Hennecke Gmbh Verfahren und Vorrichtung zur Herstellung geschäumter Polyurethan-Formkörper
DE10258546A1 (de) * 2002-12-14 2004-07-08 Stankiewicz Gmbh Verfahren und Vorrichtung zur Herstellung geschäumter Polyurethan-Formkörper
DE102004028803A1 (de) * 2004-06-15 2006-01-12 Stankiewicz Gmbh Verfahren und Vorrichtung zur Herstellung hinterschäumter luftdurchlässiger textiler Produkte
CN110171093A (zh) * 2019-06-20 2019-08-27 滁州益佳模具设备制造有限公司 一种均匀上料混合注射的生产用发泡注塑模具

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8314010D0 (en) * 1983-05-20 1983-06-29 Unifoam Ag Polymeric foam
CA1290895C (fr) * 1986-12-25 1991-10-15 Sadao Kumasaka Methode et appareil de production de mousse polyurethanne
BE1004588A3 (nl) * 1990-09-14 1992-12-15 Recticel Werkwijze voor het vervaardigen van soepel polyurethaanschuim.
US5456586A (en) 1993-07-07 1995-10-10 Carson; Scott Apparatus for manufacturing articles made of polyurethane

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2613719A1 (de) * 1976-03-31 1977-10-06 Krauss Maffei Ag Vorrichtung zum herstellen von formkoerpern aus einem gemisch von kunststoffkomponenten
DE2647482A1 (de) * 1976-10-21 1978-04-27 Bayer Ag Verfahren zur herstellung von kalthaertenden, urethangruppen aufweisenden schaumstoffen

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2613719A1 (de) * 1976-03-31 1977-10-06 Krauss Maffei Ag Vorrichtung zum herstellen von formkoerpern aus einem gemisch von kunststoffkomponenten
DE2647482A1 (de) * 1976-10-21 1978-04-27 Bayer Ag Verfahren zur herstellung von kalthaertenden, urethangruppen aufweisenden schaumstoffen

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENTS ABSTRACTS OF JAPAN Vol. 1, No. 84, 6 August 1977, page 1800C77 & JP-A-52 047896. *

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0044226A1 (fr) * 1980-07-15 1982-01-20 Brian James Blackwell Procédé de préparation de matière plastique en mousse
WO1982000297A1 (fr) * 1980-07-15 1982-02-04 J Blackwell Production d'un materiau de mousse de plastique synthetique
EP0604595A4 (fr) * 1992-01-09 1995-05-10 Scott Carson Procede et dispositif servant a fabriquer des articles en polyurethane.
DE19701728A1 (de) * 1997-01-20 1998-07-23 Hennecke Gmbh Verfahren und Vorrichtung zur Herstellung geschäumter Polyurethan-Formkörper
DE19701728C2 (de) * 1997-01-20 1998-12-10 Hennecke Gmbh Verfahren und Vorrichtung zur Herstellung geschäumter Polyurethan-Formkörper
DE10258546A1 (de) * 2002-12-14 2004-07-08 Stankiewicz Gmbh Verfahren und Vorrichtung zur Herstellung geschäumter Polyurethan-Formkörper
DE10258546B4 (de) * 2002-12-14 2005-03-10 Stankiewicz Gmbh Verfahren und Vorrichtung zur Herstellung geschäumter Polyurethan-Formkörper
DE102004028803A1 (de) * 2004-06-15 2006-01-12 Stankiewicz Gmbh Verfahren und Vorrichtung zur Herstellung hinterschäumter luftdurchlässiger textiler Produkte
US8142696B2 (en) 2004-06-15 2012-03-27 Stankiewicz Gmbh Method and device for the production of back-foamed air-permeable textile products
CN110171093A (zh) * 2019-06-20 2019-08-27 滁州益佳模具设备制造有限公司 一种均匀上料混合注射的生产用发泡注塑模具
CN110171093B (zh) * 2019-06-20 2021-04-16 滁州益佳模具设备制造有限公司 一种均匀上料混合注射的生产用发泡注塑模具

Also Published As

Publication number Publication date
EP0023749B1 (fr) 1983-07-06
ES8101990A1 (es) 1980-12-16
ES492994A0 (es) 1980-12-16
DE3064017D1 (en) 1983-08-11

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